CN108816220A - A kind of electric-bag complex dust collector and processing method - Google Patents
A kind of electric-bag complex dust collector and processing method Download PDFInfo
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- CN108816220A CN108816220A CN201810662856.3A CN201810662856A CN108816220A CN 108816220 A CN108816220 A CN 108816220A CN 201810662856 A CN201810662856 A CN 201810662856A CN 108816220 A CN108816220 A CN 108816220A
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- 239000000428 dust Substances 0.000 title claims abstract description 56
- 238000003672 processing method Methods 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 claims abstract description 40
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 13
- 239000010970 precious metal Substances 0.000 claims abstract description 13
- 230000000740 bleeding effect Effects 0.000 claims abstract description 10
- 239000003381 stabilizer Substances 0.000 claims abstract description 10
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 9
- 238000005470 impregnation Methods 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims abstract description 7
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 6
- 150000001298 alcohols Chemical class 0.000 claims abstract description 5
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 238000001035 drying Methods 0.000 claims abstract description 5
- 239000002243 precursor Substances 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims description 9
- 230000007062 hydrolysis Effects 0.000 claims description 8
- 238000006460 hydrolysis reaction Methods 0.000 claims description 8
- 239000003112 inhibitor Substances 0.000 claims description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical group CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N acetone Substances CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 4
- 150000002191 fatty alcohols Chemical group 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 4
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 4
- -1 toluoyl acetone Chemical compound 0.000 claims description 4
- 229960000583 acetic acid Drugs 0.000 claims 1
- 230000008595 infiltration Effects 0.000 claims 1
- 238000001764 infiltration Methods 0.000 claims 1
- 150000002576 ketones Chemical class 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 12
- 239000003054 catalyst Substances 0.000 abstract description 12
- 238000007598 dipping method Methods 0.000 abstract description 12
- 239000003546 flue gas Substances 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 7
- 229910052720 vanadium Inorganic materials 0.000 abstract description 5
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract description 5
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 231100000331 toxic Toxicity 0.000 abstract description 4
- 230000002588 toxic effect Effects 0.000 abstract description 4
- YRKCREAYFQTBPV-UHFFFAOYSA-N acetylacetone Chemical group CC(=O)CC(C)=O YRKCREAYFQTBPV-UHFFFAOYSA-N 0.000 description 12
- 239000012717 electrostatic precipitator Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000002341 toxic gas Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 2
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 229960000935 dehydrated alcohol Drugs 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 230000000875 corresponding effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Filtering Materials (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a kind of electric-bag complex dust collector and processing methods, including：3-4 parts of butyl titanates are dissolved in 5-6 parts of dehydrated alcohols by volume, be stirred continuously and 2-3 parts of stabilizers, obtained solution A is added；2-3 parts of noble metal precursor body reagents are added in 13-15 parts of ether by volume and are stirred continuously, and 3-5 parts of bleeding agents are added, precious metal solution B is made；The solution A is poured into the solution B, stirs evenly and solution C is made；Filter bag is submerged into the solution C and carries out vacuum impregnation；It will be heat-treated after the filter bag impregnated drying, obtain the filter bag of noble-metal-supported after cooling.Noble metal is supported on the filter bag of bag filter by the methods of dipping by the method for dipping in the present invention, therefore, denitration process can be carried out to flue gas in the precious metal catalyst effect being supported on filter bag in dust removal process, carry out denitration while realizing flue gas ash removal.The disadvantage that catalytic component based on vanadium can be overcome toxic using precious metal material.
Description
Technical field
The present invention relates to atmosphere dedusting technology fields, more specifically to a kind of electric-bag complex dust collector and processing
Method.
Background technique
NOx has become global environmental problem, SCR technology to the pollution problem of atmospheric environment
It (SCR) be current for removing nitrogen oxides in effluent is most extensively also most effective technology.Coal-burning power plant of China uses at present
Most of the process flow of smoke gas treatment technology be dedusting finally desulfurization again after first denitration, this process is in practical engineering application
In have certain problems.Before SCR reactor is usually arranged in deduster in practical application in industry, exist in high-temperature flue gas
A large amount of dust can catalyst surface formed heap ash, result in blockage and wear to catalyst, reduce catalyst denitration effect
Rate, high dirt SCR arrangement also result in the corrosion and abrasion of air preheater.
The deduster that coal-fired plant flue gas dedusting at present mostly uses greatly has electrostatic precipitator and bag filter and electric bag multiple
Close deduster.Enter electrostatic precipitator after the flue gas of SCR reaction flows through air preheater, the temperature of flue gas, which is declined, about to be tieed up
It holds at 130 DEG C or so, this temperature is unfavorable for trapping of the electrostatic precipitator specific resistance to grit, while the ammonia excessively escaped and three
Sulfur oxide also results in that electrostatic precipitator incrustation is serious, greatly reduces the efficiency of dust collection of electrostatic precipitator.Though bag filter
So than wide in industrial application, but itself is more sensitive to the temperature of receiving, and more in flue gas moisture content or take powder
Dirt has in stronger hygroscopic situation, is easy to cause filter bag to cohere, blocks the problems such as filtrate.
Prior art discloses a kind of preparation method of activated carbon supported catalyst dedusting denitrification integral fiber, this method
It is middle will in viscose rayon or polyacrylonitrile fibre impregnation catalyst agent, by low-temperature zone oxidation, nitrogen sealing high temperature furnace in by
Denitration dust collecting of the fibrous material for catalyst in flue gas is made after step heating carbonization and steam activation, although by above-mentioned side
Integrated fiber made from case can be improved the effect of dust suction or denitration.But the catalyst used in denitrification process is vanadium base
Catalyst can generate poison gas, threaten operator's life security.
Therefore, how a kind of electric-bag complex dust collector in dedusting and denitration while the generation that avoids toxic gas is provided,
The technical problem urgently to be resolved as those skilled in the art.
Summary of the invention
In view of this, the technical problem to be solved by the present invention is to how provide one kind in dedusting and denitration while having avoided
The electric-bag complex dust collector of the generation of poisonous gas, for this purpose, the present invention provides a kind of electric-bag complex dust collector and processing methods.
To achieve the above object, the present invention provides the following technical solutions：
A kind of processing method of electric-bag complex dust collector, including：
3-4 parts of butyl titanates are dissolved in 5-6 parts of dehydrated alcohols by volume, be stirred continuously and 2-3 parts of stabilizations are added
Agent, obtained solution A；
2-3 parts of noble metal precursor body reagents are added in 13-15 parts of ether by volume and are stirred continuously, and are added 3-5 parts
Precious metal solution B is made in bleeding agent；
The solution A is poured into the solution B, stirs evenly and solution C is made；
Filter bag is submerged into the solution C and carries out vacuum impregnation；
It will be heat-treated after the filter bag impregnated drying, obtain the filter bag of noble-metal-supported after cooling.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, volume ratio is added during obtained solution A
For 2.5-3 parts of hydrolysis inhibitors.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the hydrolysis inhibitor is acetic acid.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the stabilizer is acetylacetone,2,4-pentanedione or toluoyl
Acetone.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the bleeding agent is fatty alcohol polyoxyethylene ether.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, mixing time during the obtained solution A
For 15min-20min.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, mixing time during the obtained solution B
For 20min-25min.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the vacuum-impregnated vacuum pressure is
450MPa-550MPa。
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the vacuum-impregnated time is 1~8 hour.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the vacuum-impregnated number is 5-7 times.
Preferably, in the processing method of above-mentioned electric-bag complex dust collector, the temperature of the heat treatment is 350 DEG C -450
DEG C, heat treatment time is 1~10 hour.
The invention also discloses a kind of electric-bag complex dust collectors, and the electric-bag complex dust collector is as described in any of the above-described
Processing method be process.
It can be seen from the above technical scheme that noble metal is passed through the methods of dipping by the method for dipping in the present invention
It is supported on the filter bag of bag filter, therefore, acting in dust removal process in the precious metal catalyst being supported on filter bag can
Denitration process is carried out to flue gas, carries out denitration while realizing flue gas ash removal.Catalytic component based on vanadium can be overcome using precious metal material
Toxic disadvantage.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is a kind of flow diagram of the processing method of electric-bag complex dust collector provided by the embodiment of the present invention；
Fig. 2 is the flow diagram of the processing method of another kind electric-bag complex dust collector provided by the embodiment of the present invention.
Specific embodiment
Core of the invention is to provide a kind of electric-bag complex dust collector and processing method, with provide it is a kind of in dedusting and
Denitration avoids the electric-bag complex dust collector of the generation of toxic gas simultaneously.
In addition, embodiments illustrated below does not play any restriction effect to the invention described in the claims content.In addition,
The full content of composition represented by following example is not limited to must as the solution of the invention described in the claims
It needs.
Referring to Fig. 1, the processing method of the electric-bag complex dust collector in the present invention includes：
Step S1,3-4 parts of butyl titanates are dissolved in 5-6 parts of dehydrated alcohols by volume, are stirred continuously and 2-3 is added
Part stabilizer, obtained solution A.The stabilizer is acetylacetone,2,4-pentanedione or toluoyl acetone, to increase the stability of solution.Above-mentioned mistake
The time stirred in journey is 15min-20min.
Step S2,2-3 parts of noble metal precursor body reagents are added in 13-15 parts of ether by volume and are stirred continuously, and added
Enter 3-5 parts of bleeding agents, precious metal solution B is made；The bleeding agent is fatty alcohol polyoxyethylene ether.Stirred in the above process when
Between be 20min-25min.
Step S3, the solution A is poured into the solution B, stirs evenly and solution C is made；
Step S4, filter bag is submerged into the solution C and carries out vacuum impregnation；Wherein, vacuum-impregnated vacuum pressure is
For 450MPa-550MPa；The vacuum-impregnated time is 1~8 hour；The vacuum-impregnated number is 5-7 times
Step S5, it will be heat-treated after the filter bag impregnated drying, obtain the filter bag of noble-metal-supported after cooling.Wherein, institute
The temperature for stating heat treatment is 350 DEG C -450 DEG C, and heat treatment time is 1~10 hour.
Noble metal is supported on the filter bag of bag filter by the methods of dipping by the method for dipping in the present invention,
Therefore, denitration process can be carried out to flue gas in the precious metal catalyst effect being supported on filter bag in dust removal process, realize cigarette
Denitration is carried out while gas dedusting.The disadvantage that catalytic component based on vanadium can be overcome toxic using precious metal material.
Referring to Fig. 2, the processing method of another electric-bag complex dust collector is also disclosed in another embodiment of the present invention,
Specifically this method includes：
Step S1,3-4 parts of butyl titanates are dissolved in 5-6 parts of dehydrated alcohols by volume, are stirred continuously and 2-3 is added
Part stabilizer and 2.5-3 parts of part hydrolysis inhibitors, obtained solution A.The stabilizer is acetylacetone,2,4-pentanedione or toluoyl acetone, to increase
The stability of solubilization liquid；Tetrabutyl titanate hydrolysis speed can be slowed down by the way that hydrolysis inhibitor is added in this method with the pH in solution
Rate.Preferably, the hydrolysis inhibitor is acetic acid；The time stirred in the above process is 15min-20min.
Step S2,2-3 parts of noble metal precursor body reagents are added in 13-15 parts of ether by volume and are stirred continuously, and added
Enter 3-5 parts of bleeding agents, precious metal solution B is made；The bleeding agent is fatty alcohol polyoxyethylene ether.Stirred in the above process when
Between be 20min-25min.
Step S3, the solution A is poured into the solution B, stirs evenly and solution C is made；
Step S4, filter bag is submerged into the solution C and carries out vacuum impregnation；Wherein, vacuum-impregnated vacuum pressure is
For 450MPa-550MPa；The vacuum-impregnated time is 1~8 hour；The vacuum-impregnated number is 5-7 times
Step S5, it will be heat-treated after the filter bag impregnated drying, obtain the filter bag of noble-metal-supported after cooling.Wherein, institute
The temperature for stating heat treatment is 350 DEG C -450 DEG C, and heat treatment time is 1~10 hour.
Noble metal is supported on the filter bag of bag filter by the methods of dipping by the method for dipping in the present invention,
Therefore, denitration process can be carried out to flue gas in the precious metal catalyst effect being supported on filter bag in dust removal process, realize cigarette
Denitration is carried out while gas dedusting.The disadvantage that catalytic component based on vanadium can be overcome toxic using precious metal material.
The invention also discloses a kind of electric-bag complex dust collectors, and the electric-bag complex dust collector is as described in any of the above-described
Processing method be process.Since the above method has said effect, electric-bag complex dust collector prepared by the above method
With corresponding effect, details are not described herein again.
Embodiment 1
A kind of processing method of electric-bag complex dust collector is disclosed in the embodiment, this method includes：
Step 1. weighs 3 parts of butyl titanate by volume, and 6 parts and 2 parts of stabilizer of dehydrated alcohol are stirred 15min, makes
Solution A；
Step 2. weighs 2 parts of chlorination palladium reagent, and 15 parts of ether are quickly stirred, and bleeding agent 3 is added in whipping process
Part, stir 15min, the solution B of system；
Step 3. pours into solution A in solution B be stirred continuously 20min after, the solution C of system；
Filter bag is immersed in solution C by step 4., carries out vacuum impregnation, vacuum pressure 500Pa, dip time 1.5
Hour, dipping time is 8 times；
Step 5. by the filter bag after the completion of dipping in dry 12 hours in 100 DEG C of baking ovens, after be placed in 400 DEG C of air it is hot
Processing 2 hours, is finally cooled to room temperature, the filter bag of noble-metal-supported is prepared.
Electric-bag complex dust collector prepared by the above method is tested at different temperature, is measured denitration efficiency and is removed
Dirt rate and and draw table one：
Table one is that summary sheet is filtered in denitration efficiency and dedusting under different temperatures
By above-mentioned test it is found that electric-bag complex dust collector prepared by the above method is between 350 DEG C to 450 DEG C, denitration
Efficiency and dedusting filter are relatively high.
Embodiment 2
A kind of processing method of electric-bag complex dust collector is disclosed in the embodiment, this method includes：
Step 1. weighs 4 parts of butyl titanate by volume, and 5 parts and 3 parts of stabilizer of dehydrated alcohol are stirred 18min, makes
Solution A；
Step 2. weighs 3 parts of nano platinum solution, and 13 parts of ether are quickly stirred, and bleeding agent is added in whipping process
5 parts, stir 20min, the solution B of system；
Step 3. pours into solution A in solution B be stirred continuously 25min after, the solution C of system；
Filter bag is immersed in solution C by step 4., carries out vacuum impregnation, vacuum pressure 500Pa, and dip time is 3 small
When, dipping time is 8 times；
Step 5. by the filter bag after the completion of dipping in dry 12 hours in 100 DEG C of baking ovens, after be placed in 400 DEG C of air it is hot
Processing 2 hours, is finally cooled to room temperature, the filter bag of noble-metal-supported is prepared.
Electric-bag complex dust collector prepared by the above method is tested at different temperature, is measured denitration efficiency and is removed
Dirt rate and and draw table two：
Table two is that summary sheet is filtered in denitration efficiency and dedusting under different temperatures
By above-mentioned test it is found that electric-bag complex dust collector prepared by the above method is between 350 DEG C to 450 DEG C, denitration
Efficiency and dedusting filter are relatively high.
The foregoing description of the disclosed embodiments enables those skilled in the art to implement or use the present invention.
Various modifications to these embodiments will be readily apparent to those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, of the invention
It is not intended to be limited to the embodiments shown herein, and is to fit to and the principles and novel features disclosed herein phase one
The widest scope of cause.
Claims (12)
1. a kind of processing method of electric-bag complex dust collector, which is characterized in that including：
3-4 parts of butyl titanates are dissolved in 5-6 parts of dehydrated alcohols by volume, are stirred continuously and are added 2-3 parts of stabilizers, are made
Obtain solution A；
2-3 parts of noble metal precursor body reagents are added in 13-15 parts of ether by volume and are stirred continuously, and 3-5 parts of infiltrations are added
Precious metal solution B is made in agent；
The solution A is poured into the solution B, stirs evenly and solution C is made；
Filter bag is submerged into the solution C and carries out vacuum impregnation；
It will be heat-treated after the filter bag impregnated drying, obtain the filter bag of noble-metal-supported after cooling.
2. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that in the process of obtained solution A
Middle addition volume ratio is 2.5-3 parts of hydrolysis inhibitors.
3. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the hydrolysis inhibitor is vinegar
Acid.
4. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the stabilizer is levulinic
Ketone or toluoyl acetone.
5. the processing method of electric-bag complex dust collector as claimed in claim 4, which is characterized in that the bleeding agent is fatty alcohol
Polyoxyethylene ether.
6. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the mistake of the obtained solution A
Mixing time is 15min-20min in journey.
7. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the mistake of the obtained solution B
Mixing time is 20min-25min in journey.
8. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the vacuum-impregnated vacuum
Pressure is 450MPa-550MPa.
9. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the vacuum-impregnated time
It is 1~8 hour.
10. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that described vacuum-impregnated time
Number is 5-7 times.
11. the processing method of electric-bag complex dust collector as described in claim 1, which is characterized in that the temperature of the heat treatment
It is 350 DEG C -450 DEG C, heat treatment time is 1~10 hour.
12. a kind of electric-bag complex dust collector, which is characterized in that the electric-bag complex dust collector is by any in claim 1 to 11
Processing method described in is process.
Priority Applications (1)
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| CN1374880A (en) * | 1999-09-22 | 2002-10-16 | 戈尔企业控股股份有限公司 | Chemically active filter material |
| CN102500183A (en) * | 2011-11-03 | 2012-06-20 | 中国华能集团清洁能源技术研究院有限公司 | Flue gas purification system capable of simultaneously realizing high-efficiency dust removal and mercury removal |
| CN103463871A (en) * | 2013-09-02 | 2013-12-25 | 安徽锦鸿环保科技有限公司 | Membrane-laminated fiberglass filter medium capable of denitration and dust removal |
| CN106132505A (en) * | 2014-03-21 | 2016-11-16 | 托普索公司 | filter bag assembly |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1374880A (en) * | 1999-09-22 | 2002-10-16 | 戈尔企业控股股份有限公司 | Chemically active filter material |
| CN102500183A (en) * | 2011-11-03 | 2012-06-20 | 中国华能集团清洁能源技术研究院有限公司 | Flue gas purification system capable of simultaneously realizing high-efficiency dust removal and mercury removal |
| CN103463871A (en) * | 2013-09-02 | 2013-12-25 | 安徽锦鸿环保科技有限公司 | Membrane-laminated fiberglass filter medium capable of denitration and dust removal |
| CN106132505A (en) * | 2014-03-21 | 2016-11-16 | 托普索公司 | filter bag assembly |
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